CN114538577B - Electrodialysis and electrodeionization combined application equipment - Google Patents
Electrodialysis and electrodeionization combined application equipment Download PDFInfo
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- CN114538577B CN114538577B CN202210179072.1A CN202210179072A CN114538577B CN 114538577 B CN114538577 B CN 114538577B CN 202210179072 A CN202210179072 A CN 202210179072A CN 114538577 B CN114538577 B CN 114538577B
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/469—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis
- C02F1/4693—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis
- C02F1/4695—Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis electrodialysis electrodeionisation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/04—Non-contaminated water, e.g. for industrial water supply for obtaining ultra-pure water
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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- Engineering & Computer Science (AREA)
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses electrodialysis and electrodeionization combined application equipment, which comprises: the ED membrane stack comprises: the device comprises a first polar water inlet, a first raw water inlet, a first concentrated water inlet, a first polar water outlet, a first raw water outlet and a first concentrated water outlet; the first polar water inlet is communicated with the first polar water outlet through a pipeline; the first raw water inlet and the first concentrated water inlet are communicated with a raw water pipe through pipelines; the first raw water outlet is communicated with the first raw water inlet through a pipeline; the EDI membrane stack comprises: the first polar water inlet, the first raw water inlet, the first concentrated water inlet, the first polar water outlet, the first raw water outlet and the first concentrated water outlet are arranged on the water tank; the second polar water inlet, the second raw water inlet and the second concentrated water inlet are respectively communicated with the first raw water outlet through pipelines; the second polar water outlet is communicated with the second polar water inlet through a pipeline; the second concentrated water outlet is communicated with the first raw water inlet through a pipeline. The device of the invention occupies small space and has high water production rate.
Description
Technical Field
The invention relates to the technical field of seawater desalination and ultrapure water preparation, in particular to electrodialysis and electrodeionization combined application equipment.
Background
With the increasing demand of industrial fresh water and ultrapure water, various countries compete to start with seawater resources, optimize the existing water treatment process, and develop more optimal water treatment technology to obtain more fresh water and ultrapure water.
The traditional seawater desalination and ultrapure water preparation technology mainly adopts a thermal method and a membrane method. The thermal method comprises a distillation method, a freezing method and the like, and is a method for separating ions from water molecules through a continuous heat exchange process to purify water. The membrane method includes reverse osmosis, nanofiltration, etc., and is a method in which ions are trapped by allowing water molecules to permeate a semi-permeable membrane by continuously applying pressure. However, the thermal method has the problems of high energy consumption, low water production rate, easy corrosion of equipment and the like; the membrane method has the problems of large operation pressure, large vibration noise, easy pollution and blockage of the membrane and the like. Although these problems are solved to some extent at present, the effect of long-term use is not negligible.
Therefore, it is an urgent need in the art to develop a combined electrodialysis and electrodeionization apparatus with small space occupation and high water production rate.
Disclosure of Invention
In view of the above, the invention provides a combined application device of electrodialysis and electrodeionization, which occupies small space and has high water production rate.
In order to achieve the purpose, the invention adopts the following technical scheme:
an electrodialysis and electrodeionization combined application apparatus, comprising:
the number of the ED membrane stacks is multiple, and the ED membrane stacks are connected in parallel through pipelines; the ED membrane stack comprises: the device comprises a first polar water inlet, a first raw water inlet, a first concentrated water inlet, a first polar water outlet, a first raw water outlet and a first concentrated water outlet; the first polar water inlet is communicated with the first polar water outlet through a pipeline; the first raw water inlet and the first concentrated water inlet are communicated with a raw water pipe through pipelines; the first raw water outlet is communicated with the first raw water inlet through a pipeline; the first concentrated water outlet is communicated with a concentrated water discharge pipe through a pipeline;
a plurality of EDI membrane stacks are arranged and connected in parallel through pipelines; the ED membrane stack and the EDI membrane stack are connected in series through a pipeline; the EDI membrane stack comprises: the first polar water inlet, the first raw water inlet, the first concentrated water inlet, the first polar water outlet, the first raw water outlet and the first concentrated water outlet are arranged on the water tank; the second polar water inlet, the second raw water inlet and the second concentrated water inlet are respectively communicated with the first raw water outlet through pipelines; the second polar water outlet is communicated with the second polar water inlet through a pipeline; the second raw water outlet is communicated with a pipeline and a pure water drain pipe; the second concentrated water outlet is communicated with the first raw water inlet through a pipeline.
The technical scheme has the advantages that the continuous preparation of fresh water and ultrapure water can be realized by connecting the ED membrane stacks in parallel, connecting the EDI membrane stacks in parallel and connecting the ED membrane stacks and the EDI membrane stacks in series, so that the occupied space of water preparation equipment can be effectively reduced; meanwhile, the recycling of the EDI membrane stack concentrated water is realized, and the water production rate of the whole water treatment system is improved.
Preferably, the raw water pipe is connected with a first circulating water tank, and an outlet of the first circulating water tank is communicated with the first raw water inlet; the first raw water outlet is communicated with an inlet of the first circulating water tank through a pipeline; the second polar water inlet, the second raw water inlet and the second concentrated water inlet are respectively communicated with the inlet of the first circulating water tank through pipelines; a sixth electromagnetic valve is arranged at the inlet of the first circulating water tank; and a seventh electromagnetic valve is arranged on a pipeline connecting the raw water pipe and the first concentrated water inlet. The first circulating water tank can carry out circulating desalination treatment on the raw water, when the produced water reaches the target salt content (namely fresh water), the EDI membrane stack is started, and the fresh water passes through the EDI membrane stack to produce high-purity water; and the concentrated water of EDI membrane stack output is collected in the second circulation tank as the raw water of ED membrane stack, and then has improved the system water efficiency of equipment.
Preferably, the second concentrated water outlet is connected with a second circulating water tank through a pipeline, and an outlet of the second circulating water tank is communicated with an inlet of the first circulating water tank through a pipeline; and an eighth electromagnetic valve is arranged at an outlet of the second circulating water tank. The second concentrated water outlet is independently connected with the second circulating water tank, so that the concentrated water of the EDI membrane stack can be collected and reserved as the raw water of the ED membrane stack.
Preferably, the outlet of the first circulating water tank is connected with a conductivity meter for monitoring the salt content. The conductivity meter can detect the salt content in water, when the salt content of the water in the first circulating water tank reaches a set value, fresh water can be obtained, an EDI membrane stack is started, high-purity water is prepared, and the accuracy of preparing the fresh water can be improved due to the arrangement of the conductivity meter.
Preferably, a first gas-water separation tank is arranged on a pipeline connecting the first polar water outlet and the first polar water inlet; and a second gas-water separation tank is arranged on a pipeline connecting the second polar water outlet with the second polar water inlet. The first gas-water separation tank is added in the circulating process of the polar water in the ED membrane stack, so that the hydrogen in the polar water in the circulating process can be reduced and eliminated, and the polar water in the ED membrane stack flows through the first polar water outlet and the first gas-water separation tank and then flows back to the first polar water inlet to realize independent circulation; and a second gas-water separation tank is added in the circulation process of the polar water in the EDI membrane stack, so that the hydrogen in the polar water in the circulation process can be reduced and eliminated, and the polar water in the EDI membrane stack flows through a second polar water outlet and the second gas-water separation tank and then flows back to a second polar water inlet to realize independent circulation.
Preferably, a first electromagnetic valve is arranged on a pipeline connecting the outlet of the first circulating water tank and the first raw water inlet. The first electromagnetic valve is used for controlling the raw water inlet amount in the ED membrane stack.
Preferably, a second electromagnetic valve is arranged on a pipeline connecting the outlet of the first circulating water tank with the second polar water inlet, the second raw water inlet and the second concentrated water inlet. The second electromagnetic valve controls the opening of the EDI membrane stack, and the second electromagnetic valve can be opened when the salt content of the water in the first circulating water tank reaches a set value.
Preferably, a third electromagnetic valve is arranged on a pipeline connecting the second polar water inlet and the second electromagnetic valve. And the third electromagnetic valve controls the water inflow of the second pole water inlet.
Preferably, a fourth electromagnetic valve is arranged on a pipeline connecting the second concentrated water outlet and the second circulating water tank. And controlling the water inflow of the polar water in the EDI membrane stack by the fourth electromagnetic valve.
Preferably, a fifth electromagnetic valve is arranged on a pipeline in parallel connection with two adjacent first polar water inlets and two adjacent first concentrated water inlets. And a fifth electromagnetic valve can control the starting number of the ED membrane stacks.
Through the technical scheme, compared with the prior art, the invention discloses and provides electrodialysis and electrodeionization combined application equipment, which has the beneficial effects that:
(1) According to the invention, a plurality of ED membrane stacks are connected in parallel, a plurality of EDI membrane stacks are connected in parallel, and the ED membrane stacks and the EDI membrane stacks are connected in series, so that the continuous preparation of fresh water and ultrapure water can be realized, the raw water is subjected to circulating desalination treatment by the first circulating water tank, when the salt content of the water in the first circulating water tank reaches a set value, the fresh water is obtained, the second electromagnetic valve is opened to start the EDI membrane stack to prepare high-purity water, the second circulating water tank is used for collecting concentrated water generated by the EDI membrane stack, and the collected concentrated water is used as the raw water of the ED membrane stack, so that the concentrated water recycling of the EDI membrane stack is realized, and the water preparation rate of the whole water treatment system is further improved;
(2) Meanwhile, the quantity of the ED membrane stacks and the EDI membrane stacks can be adjusted according to the use condition, the occupied area of the equipment is small, and the occupied space can be saved.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
Fig. 1 is a schematic structural diagram of the apparatus provided by the present invention.
Wherein, in the figure, the position of the main body,
1-ED membrane stack;
11-a first polar water inlet; 12-a first raw water inlet; 13-a first concentrate inlet; 14-a first polar water outlet; 15-a first raw water outlet; 16-a first concentrated water outlet; 17-a first gas-water separation tank;
2-a raw water pipe; 3-a concentrated water drain pipe;
4-EDI membrane stack;
41-a second water inlet; 42-a second raw water inlet; 43-a second concentrated water inlet; 44-a second pole water outlet; 45-a second raw water outlet; 46-a second concentrated water outlet; 47-a second gas-water separation tank;
5-a pure water drain pipe; 6-a first circulation water tank; 7-a conductivity meter; 8-a first solenoid valve; 9-a second solenoid valve; 10-a third solenoid valve; 011 a fourth electromagnetic valve; 012-fifth solenoid valve; 013-a second circulating water tank; 014-sixth solenoid valve; 015-seventh solenoid valve; 016-eighth solenoid valve.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be obtained by a person skilled in the art without making any creative effort based on the embodiments in the present invention, belong to the protection scope of the present invention.
The embodiment of the invention discloses electrodialysis and electrodeionization combined application equipment, which comprises:
a plurality of ED membrane stacks 1 are arranged, and the ED membrane stacks 1 are connected in parallel through pipelines; the ED membrane stack 1 comprises: a first polar water inlet 11, a first raw water inlet 12, a first concentrated water inlet 13, a first polar water outlet 14, a first raw water outlet 15 and a first concentrated water outlet 16; the first polar water inlet 11 is communicated with the first polar water outlet 14 through a pipeline; the first raw water inlet 12 and the first concentrated water inlet 13 are communicated with the raw water pipe 2 through pipelines; the first raw water outlet 15 is communicated with the first raw water inlet 12 through a pipeline; the first concentrated water outlet 16 is communicated with the concentrated water discharge pipe 3 through a pipeline;
a plurality of EDI membrane stacks 4 are arranged, and the EDI membrane stacks 4 are connected in parallel through pipelines; the ED membrane stack 1 and the EDI membrane stack 4 are connected in series through a pipeline; the EDI membrane stack 4 comprises: a second dipolar water inlet 41, a second raw water inlet 42, a second concentrated water inlet 43, a second dipolar water outlet 44, a second raw water outlet 45, and a second concentrated water outlet 46; the second polar water inlet 41, the second raw water inlet 42 and the second concentrated water inlet 43 are respectively communicated with the first raw water outlet 45 through pipelines; the second polar water outlet 44 is communicated with the second polar water inlet 41 through a pipeline; the second raw water outlet 45 is communicated with the pipeline and the pure water drain pipe 5; the second concentrated water outlet 46 is communicated with the first raw water inlet 12 through a pipeline. According to the invention, the quantity of the ED membrane stacks 1 and the EDI membrane stacks 4 can be self-adaptively configured according to the actual water treatment capacity, the plurality of ED membrane stacks 1 are connected in parallel to realize seawater circulating desalination, and the plurality of EDI membrane stacks 4 are connected in parallel to realize organic combination of ultrapure water preparation, so that the occupied space of the whole set of equipment of the commonly used series ED membrane stacks 1 and series EDI membrane stacks 4 can be obviously reduced, and the water treatment efficiency is obviously improved; meanwhile, the recycling of the concentrated water of the EDI membrane stack 4 also improves the water production efficiency of the whole water treatment system.
In order to further optimize the technical scheme, the raw water pipe 2 is connected with a first circulating water tank 6, and an outlet of the first circulating water tank 6 is communicated with a first raw water inlet 12; the first raw water outlet 15 is communicated with an inlet of the first circulating water tank 6 through a pipeline; the second polar water inlet 41, the second raw water inlet 42 and the second concentrated water inlet 43 are respectively communicated with the inlet of the first circulating water tank 6 through pipelines; a sixth electromagnetic valve 014 is arranged at the inlet of the first circulating water tank 6; a seventh electromagnetic valve 015 is arranged on a pipeline connecting the raw water pipe 2 and the first concentrated water inlet 13.
In order to further optimize the technical scheme, the second concentrated water outlet 46 is connected with a second circulating water tank 013 through a pipeline, and the outlet of the second circulating water tank 013 is communicated with the inlet of the first circulating water tank 6 through a pipeline; an outlet of the second circulating water tank 013 is provided with an eighth solenoid valve 016. The water that second dense water export 46 department flows out directly gets into solitary second circulation tank 013, collects the dense water of EDI membrane stack 4, reserves the raw water of ED membrane stack 1, realizes the dense water retrieval and utilization of EDI membrane stack 4.
In order to further optimize the above solution, the outlet of the first circulation water tank 6 is connected to a conductivity meter 7 for monitoring the salt content. First circulation tank 6 cooperatees with conductivity meter 7, can circulate desalination by water to can monitor the salt content in water in real time, and then more accurate to the detection of water.
In order to further optimize the technical scheme, a first gas-water separation tank 17 is arranged on a pipeline connecting the first polar water outlet 14 and the first polar water inlet 11; a second gas-water separation tank 47 is arranged on a pipeline connecting the second polar water outlet 44 and the second polar water inlet 41.
In order to further optimize the above technical solution, a first electromagnetic valve 8 is disposed on a pipeline connecting an outlet of the first circulation water tank 6 and the first raw water inlet 12.
In order to further optimize the above technical solution, a second electromagnetic valve 9 is disposed on a pipeline connecting an outlet of the first circulating water tank 6 with the second extreme water inlet 41, the second raw water inlet 42, and the second concentrated water inlet 43.
In order to further optimize the above technical solution, a third electromagnetic valve 10 is disposed on a pipeline connecting the second pole water inlet 41 and the second electromagnetic valve 9.
In order to further optimize the above technical solution, a fourth solenoid valve 011 is provided on a pipeline connecting the second concentrated water outlet 44 and the second circulation tank 013.
In order to further optimize the above technical solution, a fifth electromagnetic valve 012 is disposed on a pipeline connecting two adjacent first polar water inlets 11 and two adjacent first concentrated water inlets 13 in parallel.
The water treatment process comprises the following steps:
water flowing out of the first polar water outlet 14 passes through the first gas-water separation tank 17 and then flows back into the ED membrane stack 1 through the first polar water inlet 11; raw water flows into a first circulating water tank 6, water in the first circulating water tank 6 flows into the ED membrane stack 1 through a first raw water inlet 12, and water flowing out of a first raw water outlet 15 flows back into the first circulating water tank 6 again; raw water enters the ED membrane stack 1 through a first concentrated water inlet 13, and then water at a first concentrated water outlet 16 is discharged through a concentrated water discharge pipe 3;
when the salt content of the water in the first circulating water tank 6 reaches a set value, closing the first electromagnetic valve 8, then opening the second electromagnetic valve 9, starting the EDI membrane stack 4, enabling the water in the first circulating water tank 6 to enter the EDI membrane stack 4 through the second polar water inlet 41, and enabling the water at the second polar water outlet 44 to flow back to the EDI membrane stack 4 through the second polar water inlet 41; water in the first circulating water tank 6 enters the EDI membrane stack 4 through a second raw water inlet 42, and high-purity water flowing out of a second raw water outlet 45 is discharged through a pure water discharge pipe 5; in water in the first circulation tank 6 entered into EDI membrane stack 4 through second dense water import 43, the water that second dense water export 46 flows out flows back to second circulation tank 013 through the pipe in, collects EDI membrane stack 4's dense water, as next time the raw water of ED membrane stack 1, and then has improved the system water efficiency of equipment.
The embodiments in the present description are described in a progressive manner, each embodiment focuses on differences from other embodiments, and the same and similar parts among the embodiments are referred to each other.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (10)
1. An electrodialysis and electrodeionization combined application apparatus, comprising:
the device comprises a plurality of ED membrane stacks (1), wherein the ED membrane stacks (1) are connected in parallel through pipelines; the ED membrane stack (1) comprises: the device comprises a first polar water inlet (11), a first raw water inlet (12), a first concentrated water inlet (13), a first polar water outlet (14), a first raw water outlet (15) and a first concentrated water outlet (16); the first polar water inlet (11) is communicated with the first polar water outlet (14) through a pipeline; the first raw water inlet (12) and the first concentrated water inlet (13) are communicated with the raw water pipe (2) through pipelines; the first raw water outlet (15) is communicated with the first raw water inlet (12) through a pipeline; the first concentrated water outlet (16) is communicated with a concentrated water discharge pipe (3) through a pipeline;
the device comprises a plurality of EDI membrane stacks (4), wherein the EDI membrane stacks (4) are connected in parallel through pipelines; the ED membrane stack (1) and the EDI membrane stack (4) are connected in series through a pipeline; the EDI membrane stack (4) comprises: a second extreme water inlet (41), a second raw water inlet (42), a second concentrated water inlet (43), a second extreme water outlet (44), a second raw water outlet (45) and a second concentrated water outlet (46); the second polar water inlet (41), the second raw water inlet (42) and the second concentrated water inlet (43) are respectively communicated with the first raw water outlet (45) through pipelines; the second diode water outlet (44) is communicated with the second diode water inlet (41) through a pipeline; the second raw water outlet (45) is communicated with a pipeline and a pure water drain pipe (5); the second concentrated water outlet (46) is communicated with the first raw water inlet (12) through a pipeline.
2. An electrodialysis and electrodeionization combined application apparatus as claimed in claim 1, wherein a first circulation water tank (6) is connected to the raw water pipe (2), and an outlet of the first circulation water tank (6) is communicated with the first raw water inlet (12); the first raw water outlet (15) is communicated with an inlet of the first circulating water tank (6) through a pipeline; the second polar water inlet (41), the second raw water inlet (42) and the second concentrated water inlet (43) are respectively communicated with an inlet of the first circulating water tank (6) through pipelines; a sixth electromagnetic valve (014) is arranged at the inlet of the first circulating water tank (6); and a seventh electromagnetic valve (015) is arranged on a pipeline connecting the raw water pipe (2) and the first concentrated water inlet (13).
3. An electrodialysis and electrodeionization combined use apparatus according to claim 2, wherein the second concentrated water outlet (46) is connected to a second circulating water tank (013) through a pipe, and an outlet of the second circulating water tank (013) is connected to an inlet of the first circulating water tank (6) through a pipe; an eighth electromagnetic valve (016) is arranged at an outlet of the second circulating water tank (013).
4. An electrodialysis and electrodeionization combined application apparatus according to claim 2, wherein the outlet of the first circulation water tank (6) is connected with a conductivity meter (7) for monitoring the salt content.
5. An electrodialysis and electrodeionization combined application apparatus as claimed in claim 1, wherein a first gas-water separation tank (17) is provided on a pipeline connecting the first polar water outlet (14) and the first polar water inlet (11); and a second gas-water separation tank (47) is arranged on a pipeline connecting the second polar water outlet (44) and the second polar water inlet (41).
6. An electrodialysis and electrodeionization combined application apparatus as claimed in claim 2 or 3, wherein a first electromagnetic valve (8) is provided on a pipeline connecting the outlet of the first circulating water tank (6) and the first raw water inlet (12).
7. An electrodialysis and electrodeionization combined application apparatus according to claim 6, wherein the second electromagnetic valve (9) is disposed on the pipeline connecting the outlet of the first circulating water tank (6) with the second polar water inlet (41), the second raw water inlet (42) and the second concentrated water inlet (43).
8. An electrodialysis and electrodeionization combined application apparatus as claimed in claim 7, wherein a third electromagnetic valve (10) is arranged on a pipeline connecting the second polar water inlet (41) and the second electromagnetic valve (9).
9. An electrodialysis and electrodeionization combined use apparatus according to claim 3, wherein a fourth solenoid valve (011) is provided on a pipe connecting the second concentrated water outlet (46) and the second circulation water tank (013).
10. The electrodialysis and electrodeionization combined application device of claim 9, wherein a fifth solenoid valve (012) is arranged on the parallel pipeline of two adjacent first polar water inlets (11) and two adjacent first concentrated water inlets (13).
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| CN202210179072.1A CN114538577B (en) | 2022-02-25 | 2022-02-25 | Electrodialysis and electrodeionization combined application equipment |
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| CN202210179072.1A CN114538577B (en) | 2022-02-25 | 2022-02-25 | Electrodialysis and electrodeionization combined application equipment |
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| CN114538577B true CN114538577B (en) | 2022-11-29 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US7744760B2 (en) * | 2006-09-20 | 2010-06-29 | Siemens Water Technologies Corp. | Method and apparatus for desalination |
| US20100006438A1 (en) * | 2008-07-11 | 2010-01-14 | Biological Targets, Inc. | Water purification process |
| CN103359854A (en) * | 2012-04-06 | 2013-10-23 | 王明亚 | Method and device for treating inorganic ammonium salt wastewater by using integrated membrane |
| JP6075030B2 (en) * | 2012-11-26 | 2017-02-08 | 三浦工業株式会社 | Pure water production equipment |
| CN103406025B (en) * | 2013-08-28 | 2016-11-09 | 中国石油化工股份有限公司 | A kind of double membrane stack-magnetoelectricity dialysis is utilized to remove the device of heat stable salts in amine desulphurization solvent continuously |
| CN111377506A (en) * | 2020-04-21 | 2020-07-07 | 九江七所精密机电科技有限公司 | EDI membrane stack and application thereof |
| CN215208906U (en) * | 2020-11-20 | 2021-12-17 | 广州高澜节能技术股份有限公司 | Electric deionization desalination device applied to high-voltage direct-current transmission valve cooling system |
| CN215559204U (en) * | 2021-09-13 | 2022-01-18 | 甘肃省膜科学技术研究院有限公司 | Special film module ware |
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